Todd,

Take a look at 2007 NFPA #14. There are many changes that effect the use
of master (4' & 6") PRV's basically making it uneconomical to use
anything other than a PRV at every hose and FCV. Whatever tricks you
have up your sleeve you better use them before the 07 #14 is adopted.

Variable speed pumps are great for warehouse applications and not so
high high-rises but are not available in high enough pressures for 25-30
story buildings.

Ron Fletcher
Aero Automatic
Phoenix, AZ

-----Original Message-----
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Bobby
McCullough
Sent: Wednesday, March 14, 2007 5:14 AM
To: [email protected]
Subject: RE: pump tricks

Tony:

I believe NFPA 20 2003 and 2007 limit the use of a main pressure relief
valve for use with a diesel pump and/or in combination with a variable
speed drive.  I don't believe the relief valve is allowed with an
electric pump just to chop off the high end of the pressure curve.

Bobby McCullough

-----Original Message-----
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of A.P.Silva
Sent: Wednesday, March 14, 2007 1:37 AM
To: [email protected]
Subject: RE: pump tricks

This is an old thread, but I'm working on two projects, a six storey and
9
storey with fire pumps and it got me thinking (not an easy feat). Most
times, the problem is not when you have a large flow through the
sprinklers or hose stations. It is when the flow is small or at churn
pressure.
When
the flow is large, the pressure has dropped down below 175 psi. When the
flow is small you don't need the extra pressure. So if you install a
pressure relief valve set at say 160 psi, you shouldn't need the XH
pipe, fittings and pressure reducing valves. I might be wrong, but I'm
thinking the pressure relief valve must be costing less than a pressure
reducing valve. Any thoughts?

Tony 

-----Original Message-----
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams
- work
Sent: February 7, 2007 7:22 AM
To: [email protected]
Subject: pump tricks

I seem to be running into several situations lately where there is a
very fine balancing act between meeting the 100 psi at the top outlet of
the standpipe and not exceeding 175 psi at the base of the riser. 
(6 story hotels are a good example) Does anybody have any good ideas
they'd care to share on making these work? I'd like to limit the use of
extra-heavy pipe and fitting (especially larger sizes) and PRVs. I have
several tricks up my sleeve, but I'm running out of sleeves.

Todd

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
860-535-2080
www.fpdc.com 

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